CN103820160A - Combustion chamber, coal water slurry gasification furnace with water wall and multiple opposite nozzles, and application of coal water slurry gasification furnace - Google Patents
Combustion chamber, coal water slurry gasification furnace with water wall and multiple opposite nozzles, and application of coal water slurry gasification furnace Download PDFInfo
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- 238000002485 combustion reaction Methods 0.000 title claims abstract description 57
- 238000002309 gasification Methods 0.000 title claims abstract description 52
- 239000002002 slurry Substances 0.000 title claims abstract description 39
- 239000003245 coal Substances 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 74
- 229910052751 metal Inorganic materials 0.000 claims abstract description 38
- 239000002184 metal Substances 0.000 claims abstract description 38
- 239000002893 slag Substances 0.000 claims abstract description 37
- 239000007789 gas Substances 0.000 claims description 27
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 13
- 239000001301 oxygen Substances 0.000 claims description 13
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- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- 239000010883 coal ash Substances 0.000 description 2
- 239000003250 coal slurry Substances 0.000 description 2
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Abstract
本发明涉及一种燃烧室及其水冷壁多喷嘴对置式水煤浆气化炉和应用,所述燃烧室包括金属炉壳(1)、盘管式水冷壁内件(2)、设于所述燃烧室顶部的预热喷嘴室(3)、工艺喷嘴室(4)、位于所述燃烧室下端中心部位的气渣出口(5);所述工艺喷嘴室(4)按水平方向分1~3层设置在所述燃烧室的上半部分空间,每一层设有1~3对所述工艺喷嘴室(4);所述盘管式水冷壁内件(2)由2~10根相同规格的金属管盘绕而成,所述金属管的进出端部与集箱连接。本发明设计的燃烧室大大拓展了水煤浆气化工艺的煤种适应范围,其部件可单独更换或维修,安装在多个工艺喷嘴室4内的工艺喷嘴可以全部或者部分工艺喷嘴进行工作,大大增加了气化炉的运行负荷范围。The invention relates to a combustion chamber and its water-cooled wall multi-nozzle opposed coal-water slurry gasification furnace and its application. The preheating nozzle chamber (3) on the top of the combustion chamber, the process nozzle chamber (4), and the gas slag outlet (5) located at the center of the lower end of the combustion chamber; the process nozzle chamber (4) is divided into 1~ 3 layers are arranged in the upper half space of the combustion chamber, and each layer is provided with 1 to 3 pairs of the process nozzle chambers (4); The standard metal pipe is coiled, and the inlet and outlet ends of the metal pipe are connected with the header. The combustion chamber designed by the present invention greatly expands the coal type adaptability range of the coal-water slurry gasification process, its components can be replaced or repaired separately, and the process nozzles installed in a plurality of process nozzle chambers 4 can work in whole or in part. The operating load range of the gasifier is greatly increased.
Description
技术领域technical field
本发明涉及一种燃烧室及其水煤浆气化炉的结构,采用水冷壁作为多喷嘴对置式水煤浆气化炉的内件衬里。The invention relates to a combustion chamber and the structure of a coal-water slurry gasification furnace. A water-cooled wall is used as the internal part lining of the multi-nozzle opposed coal-water slurry gasification furnace.
背景技术Background technique
气流床水煤浆气化技术近年来已经获得广泛应用。其中有代表性的技术包括美国GE公司的水煤浆气化技术(原Texaco水煤浆气化技术)、华东理工大学开发的多喷嘴对置式煤气化技术(中国专利,专利号ZL98110616.1,ZL2005101114824.8,ZL01210097.8)。Entrained bed coal-water slurry gasification technology has been widely used in recent years. Among them, representative technologies include the coal-water slurry gasification technology of GE Company of the United States (formerly Texaco coal-water slurry gasification technology), and the multi-nozzle opposed coal gasification technology developed by East China University of Science and Technology (Chinese patent, patent number ZL98110616.1, ZL2005101114824.8, ZL01210097.8).
传统的气流床水煤浆气化技术一般采用以耐火砖及隔热保温材料作为气化炉燃烧室隔热衬里。这种气化炉燃烧室的衬里形式具有高温保护及蓄热、隔热作用。Traditional entrained bed coal-water slurry gasification technology generally uses refractory bricks and thermal insulation materials as the thermal insulation lining of the combustion chamber of the gasifier. The lining form of the combustion chamber of the gasifier has the functions of high temperature protection, heat storage and heat insulation.
耐火砖形式的燃烧室衬里主要存在以下几点不足:The combustion chamber lining in the form of refractory bricks mainly has the following shortcomings:
1、对水煤浆气化的原料煤有限制。目前,传统的以耐火砖为衬里的水煤浆气化炉,一般采用灰熔融温度较低的烟煤作为气化煤原料。之所以采用灰熔融温度较低的煤,是因为气流床气化炉一般都采用液态排渣的方式,要使煤灰变成液态渣,就需要气化区温度高于灰熔融温度以将煤灰烧熔。但是,气化温度过高,会大大加剧耐火衬里材料的蚀损,为了保证一定的耐火衬里材料使用寿命,就不得不采用灰熔融温度较低的煤,这大大限制了中国广泛存在的高灰融点煤在水煤浆气化工艺中的适用性。1. There are restrictions on raw coal for coal-water slurry gasification. At present, traditional coal-water slurry gasifiers lined with refractory bricks generally use bituminous coal with a low ash melting temperature as the gasification coal raw material. The reason why coal with a lower ash melting temperature is used is that entrained bed gasifiers generally adopt the method of liquid slag removal. To turn coal ash into liquid slag, the temperature in the gasification zone needs to be higher than the ash melting temperature to remove the coal ash. Ashes melted. However, if the gasification temperature is too high, the corrosion of the refractory lining material will be greatly aggravated. In order to ensure a certain service life of the refractory lining material, coal with a lower ash melting temperature has to be used, which greatly limits the high ash that widely exists in China. Applicability of melting point coal in coal water slurry gasification process.
2、耐火砖需要定期更换,费用高,环境问题较大。即使采用适宜的水煤浆气化用煤(指灰熔点较低),耐火砖衬里,尤其是最内层抗高温的耐火砖,由于其受到高温气渣的侵蚀、冲刷,在使用一段时间后,就需要对局部或者整体耐火砖衬里进行更换。这一方面增加了企业的运行成本,另外,由于目前的耐火砖材料基本采用铬作为主要原料,而铬的制备熔融等过程带来严重的环境问题。2. Refractory bricks need to be replaced regularly, which leads to high costs and serious environmental problems. Even if suitable coal for coal-water slurry gasification (referring to low melting point of ash), the refractory brick lining, especially the innermost high-temperature resistant refractory brick, will be damaged after a period of use due to the erosion and erosion of high-temperature gas slag. , it is necessary to replace the partial or overall refractory brick lining. On the one hand, this increases the operating cost of the enterprise. In addition, since the current refractory brick materials basically use chromium as the main raw material, the preparation and melting of chromium brings serious environmental problems.
耐火砖需要预热,增加了运行成本,减少了设备可利用率。Refractory bricks need to be preheated, which increases operating costs and reduces equipment availability.
发明内容Contents of the invention
本发明的主要目的是提供一种以水冷壁为水煤浆气化炉燃烧室衬里的技术,以解决传统的以耐火砖为衬里的水煤浆气化炉燃烧室存在的弊端。The main purpose of the present invention is to provide a kind of technology that uses water wall as the combustion chamber lining of coal-water slurry gasifier to solve the disadvantages of the traditional combustion chamber of coal-water slurry gasifier that uses refractory bricks as the lining.
一种燃烧室,所述燃烧室包括金属炉壳1、盘管式水冷壁内件2、设于所述燃烧室顶部的预热喷嘴室3、工艺喷嘴室4、位于所述燃烧室下端中心部位的气渣出口5;A combustion chamber, which includes a
所述工艺喷嘴室4按水平方向分1~3层(每一层的工艺喷嘴室4位于同一水平面)设置在所述燃烧室的上半部分空间,每一层设有1~3对所述工艺喷嘴室4,且每一层的所述工艺喷嘴室4在所述气化炉的圆周方向上均匀布置;The
所述盘管式水冷壁内件2由2~10根相同规格的金属管盘绕而成,所述金属管的进出端部与集箱连接;所述盘管式水冷壁内件2的竖直轴线与所述金属炉壳1的竖直轴线重合;The coil-type water-cooled
所述气渣出口5与所述燃烧室在竖直方向上同轴,并且,所述气渣出口5由1~5根金属管盘绕而成。The gas slag outlet 5 is coaxial with the combustion chamber in the vertical direction, and the gas slag outlet 5 is formed by coiling 1 to 5 metal pipes.
所述预热喷嘴室3与所述金属炉壳1的竖直轴线重合,并且,所述预热喷嘴室3由1~5根金属管盘绕而成。The preheating
所述预热喷嘴室3与所述盘管式水冷壁内件2之间具有用弹性轻质耐火材料填充的缝隙。There is a gap filled with elastic light refractory material between the preheating
所述气渣出口5与所述盘管式水冷壁内件2之间具有用弹性轻质耐火材料填充的缝隙。There is a gap filled with elastic light refractory material between the gas slag outlet 5 and the coiled water-cooled wall
所述工艺喷嘴室4包括所述金属炉壳1的炉壳水平孔6和所述盘管式水冷壁内件2的水冷壁水平孔7,所述炉壳水平孔6与所述水冷壁水平孔7之间通过波纹管9互相联接,所述炉壳水平孔6、水冷壁水平孔7的水平中心轴线互相平行。The
一种水冷壁多喷嘴对置式水煤浆气化炉,具有以上任一所述的燃烧室。A water-cooled wall multi-nozzle opposed coal-water slurry gasifier has any one of the above-mentioned combustion chambers.
上述水冷壁多喷嘴对置式水煤浆气化炉的应用,具体为:将所述气化炉用于水煤浆进料气流床的气化,包括如下步骤:通过安装于工艺喷嘴室4的工艺喷嘴将水煤浆气化原料和氧气喷入所述燃烧室,进行气化反应,生成的高温气体及高温熔渣向下流动,经过所述气渣出口5排出所述燃烧室。The application of the above-mentioned multi-nozzle opposed coal-water slurry gasifier with a water wall is specifically: using the gasifier for the gasification of the coal-water slurry feed entrained flow bed, including the following steps: The process nozzle sprays coal-water slurry gasification raw materials and oxygen into the combustion chamber for gasification reaction, and the generated high-temperature gas and high-temperature slag flow downward and are discharged from the combustion chamber through the gas slag outlet 5 .
在所述气化反应的初期,通过所述预热喷嘴室3内安装的预热喷嘴喷入气态或液态的燃料和氧化剂(例如,空气等),进行燃烧反应,使所述盘管式水冷壁内件2进行预热;当所述盘管式水冷壁内件2预热到指定温度时,再将所述水煤浆气化原料和所述氧气通过安装于工艺喷嘴室4的工艺喷嘴喷入所述燃烧室并由所述预热喷嘴的火焰点燃;待所述工艺喷嘴的火焰稳定后,熄灭所述预热喷嘴的火焰。In the initial stage of the gasification reaction, gaseous or liquid fuel and oxidant (for example, air, etc.) are sprayed into the preheating nozzle installed in the preheating
在所述工艺喷嘴全部或者部分已经建立起与所述水煤浆气化原料和氧气的稳定火焰,并熄灭所述预热喷嘴的火焰后,继续通入氮气、二氧化碳、水蒸汽中的单一或混合气体,或者继续通入新的水煤浆气化原料和氧气作为气化进料,或者通入气化反应所产生的混合气;After all or part of the process nozzle has established a stable flame with the coal-water slurry gasification raw material and oxygen, and extinguished the flame of the preheating nozzle, continue to feed nitrogen, carbon dioxide, steam or Mixed gas, or continue to feed new coal-water slurry gasification raw materials and oxygen as gasification feed, or feed mixed gas generated by gasification reaction;
其中,当所述工艺喷嘴的部分喷入所述水煤浆气化原料和氧气进行气化反应时,所述工艺喷嘴的其他部分喷入少量氮气、二氧化碳、水蒸汽中的单一或者混合气体,以保护工艺喷嘴不被气化反应形成的高温所损坏。Wherein, when part of the process nozzle is injected into the coal-water slurry gasification raw material and oxygen for gasification reaction, other parts of the process nozzle are injected with a small amount of single or mixed gases in nitrogen, carbon dioxide, and water vapor, To protect the process nozzle from being damaged by the high temperature formed by the gasification reaction.
与传统的以耐火砖为衬里的水煤浆气化技术相比,本发明具有以下显著优点:Compared with the traditional coal-water slurry gasification technology lined with refractory bricks, the present invention has the following significant advantages:
1、采用水冷壁作为水煤浆气化炉内部结构,利用水冷壁“以渣抗渣”的特点,可气化灰熔融温度较高的煤,大大拓展了水煤气化工艺的煤种适应范围。1. The water-cooled wall is used as the internal structure of the coal-water slurry gasifier, and the characteristics of "resisting slag with slag" of the water-cooled wall can be used to gasify coal with a high ash melting temperature, which greatly expands the coal type application range of the water-coal gasification process.
2、采用盘管式水冷壁2作为气化炉燃烧室主体内部结构,顶部的预热喷嘴室3、侧置的工艺喷嘴室4及下部的气渣出口5与盘管式水冷壁之间不直接固定连接,间隙处用弹性轻质耐火材料填充。这样,后三者都可以与盘管式水冷壁脱离,单独更换或维修。一方面提高了相关部件的使用可靠性,另一方面也最大程度降低了水冷壁主体的故障率和维修工作量。2. The coil-type water-cooled
3、采用安装在顶部预热喷嘴室3内的预热喷嘴对气化炉燃烧室内部进行预热,并提供稳定火焰点燃安装在工艺喷嘴室4内的工艺喷嘴喷入的煤浆和氧气,不需要在同一个喷嘴内进行预燃火焰和煤浆氧气工艺进料的切换,使得水煤浆气化炉开车过程简单可靠。3. Use the preheating nozzle installed in the top preheating
4、安装在多个工艺喷嘴室4内的工艺喷嘴,可以全部或者部分工艺喷嘴进行工作,大大增加了气化炉的运行负荷范围。4. The process nozzles installed in multiple
附图说明Description of drawings
图1是水冷壁多喷嘴对置式水煤浆气化炉中燃烧室的结构示意图;Fig. 1 is the structural representation of the combustion chamber in the multi-nozzle opposed type coal-water slurry gasifier with water wall;
图2是盘管式水冷壁内件的结构示意图。Fig. 2 is a structural schematic diagram of the inner part of the coiled water-cooled wall.
符号说明:Symbol Description:
1金属炉壳;2盘管式水冷壁内件;3预热喷嘴室;4工艺喷嘴室;1 Metal furnace shell; 2 Coil water-cooled wall internals; 3 Preheating nozzle chamber; 4 Process nozzle chamber;
5气渣出口;6炉壳水平孔;7水冷壁水平孔,8工艺喷嘴;5 gas slag outlet; 6 horizontal hole in the furnace shell; 7 horizontal hole in the water wall, 8 process nozzle;
9波纹管;10定位块;11水冷壁盘管进水管;9 bellows; 10 positioning block; 11 water wall coil inlet pipe;
12水冷壁盘管出水管;13预热喷嘴;14弹性轻质耐火材料;12 water wall coil outlet pipe; 13 preheating nozzle; 14 elastic light refractory material;
15预热喷嘴开口;16气渣出口开口。15 preheating nozzle opening; 16 air slag outlet opening.
具体实施方式Detailed ways
下面将结合实施例进一步阐明本发明的内容,但这些实施例并不限制本发明的保护范围。The content of the present invention will be further illustrated below in conjunction with examples, but these examples do not limit the protection scope of the present invention.
实施例1Example 1
如图1所示,水冷壁多喷嘴对置式水煤浆气化炉中燃烧室具有金属炉壳1,其主体为筒状结构,金属炉壳1的上部为一球形封头、下部为圆锥状结构。该金属炉壳1的下部可联接一个同径或者异径的气化洗涤冷却设备或者热回收设备。球形封头中心、筒体直段及圆锥状下部的下端设置圆形开口,以分别作为预热喷嘴13、工艺喷嘴8及气渣出口5的安装位置。As shown in Figure 1, the combustion chamber in the water-wall multi-nozzle opposed coal-water slurry gasifier has a
燃烧室还具有盘管式水冷壁内件2、设于燃烧室顶部的预热喷嘴室3、工艺喷嘴室4、位于燃烧室下端中心部位的气渣出口5。The combustion chamber also has a coil-type water-cooled wall
为了确保热胀冷缩过程中盘管式水冷壁内件2与金属炉壳1之间保持一定距离,设置了定位块10。In order to ensure a certain distance between the coiled water-cooled wall
工艺喷嘴室4按水平方向分1~3层设置在燃烧室的上半部分空间,每一层设有1~3对工艺喷嘴室4,即,同一层的工艺喷嘴室4位于同一水平面,且同一层的工艺喷嘴室4在气化炉的圆周方向上均匀布置;The
气渣出口5与燃烧室在竖直方向上同轴,由1~5根金属管盘绕而成。The gas slag outlet 5 is coaxial with the combustion chamber in the vertical direction, and is formed by coiling 1 to 5 metal pipes.
预热喷嘴室3与金属炉壳1的竖直轴线重合,由1~5根金属管盘绕而成。预热喷嘴室3设置在燃烧室顶部中心处,由一个独立可拆卸的由金属管盘绕而成的筒形结构并以同轴的方式安装于盘管式水冷壁内件2顶部开口空间内形成。采用本发明设计的预热喷嘴室3结构,可以独立更换检修预热喷嘴室,而不影响主体水冷壁盘管。The preheating
预热喷嘴室3与盘管式水冷壁内件2之间以及气渣出口5与盘管式水冷壁内件2之间具有用弹性轻质耐火材料14填充的缝隙(3~200mm)。There are gaps (3-200 mm) filled with elastic light
工艺喷嘴室4包括金属炉壳1的炉壳水平孔6和盘管式水冷壁内件2的水冷壁水平孔7,炉壳水平孔6与水冷壁水平孔7之间通过波纹管9互相联接,炉壳水平孔6、水冷壁水平孔7的水平中心轴线互相平行。The
工艺喷嘴室4设计在燃烧室直段的侧面,如前所述,在与金属炉壳1和水冷壁盘管2相对应的位置上均有开口空间,在开口空间内形成由一个独立可拆卸的由金属管盘绕而成的筒形结构,该筒形结构为与水冷壁盘管2开口的中心轴平行的工艺喷嘴室内筒。但是,在冷态安装时,工艺喷嘴室内筒的中心轴略低于水冷壁盘管2开口的中心轴,这是考虑盘管式水冷壁内件2在热态状态下膨胀后,其开口中心轴与内筒中心轴尽量共轴。工艺喷嘴室内筒在靠近金属炉壳1一侧与波纹管9及一个同径短接管固定,短接管通过焊接的方式固定在金属炉壳1上。通过波纹管9,可消除由于热胀冷缩效应造成的工艺喷嘴室内筒与其固定端之间的应力。工艺喷嘴室内筒与主体水冷壁盘管之间预留一定的间隙(3~200mm),间隙空间内用弹性轻质耐火材料填充。工艺喷嘴室内筒可独立拆卸检修,而不影响主体水冷壁盘管。The
气渣出口5位于盘管式水冷壁内件2下部锥底中心处。气渣出口5由一个独立可拆卸的由金属管盘绕而成的筒形结构形成气渣出口内筒,气渣出口内筒与盘管式水冷壁内件2下部的气渣出口5的开口空间同轴,且有一定的间隙(3~200mm),间隙空间内用弹性轻质耐火材料填充。气渣出口内筒可独立拆卸检修,而不影响盘管式水冷壁内件2。The air slag outlet 5 is located at the center of the cone bottom at the lower part of the coil-type water-cooled wall
如图2所示的盘管式水冷壁内件,其主体为一个盘管式结构。所谓盘管式,是若干根(本发明为2~10根,优选3~5根)金属管平行螺旋盘绕而成,并在相应的位置留出预热喷嘴室3、工艺喷嘴室4及气渣出口5的开口空间(图中示出了预热喷嘴开口15和气渣出口开口16)。为了保护金属盘管,可在靠近炉膛一侧的金属盘管表面敷设一层0.5~200mm厚的隔热耐火材料,如碳化硅。当气化炉燃烧室内发生水煤浆气化反应过程时,煤中的灰渣在高温下熔融,部分灰渣粘附到水冷壁表面后被冷却固化,从而形成一个动态保护层,以保护水冷壁盘管不被高温烧蚀。这一动态渣层随着煤种和气化温度的不同而发生厚度的改变,但总体上,从水冷壁盘管壁面向炉膛内依次为:固态渣层、软化渣层和流动渣层。As shown in Fig. 2, the coil type water-cooled wall inner part has a main body of a coil type structure. The so-called coiled tube type is formed by a number of metal tubes (2 to 10 in the present invention, preferably 3 to 5) that are spirally coiled in parallel, and the preheating
平行螺旋盘绕的金属管的进出端部与集箱连接;盘管式水冷壁内件2的竖直轴线与所述金属炉壳1的竖直轴线重合,具有水冷壁盘管进水管11和水冷壁盘管出水管12。The inlet and outlet ends of parallel helically coiled metal pipes are connected to the header; the vertical axis of the coiled water-cooled wall
按照本发明设计的气化炉燃烧室,具有开工点火快捷稳定的特点。通过设置在顶部的预热喷嘴室内的预热喷嘴,用柴油、天然气、液化气、工厂驰放气或者其他气液态燃料,与空气进行燃烧反应,首先对主体水冷壁盘管进行预热,然后通过设置在工艺喷嘴室内的工艺喷嘴,喷入水煤浆和氧气,被预热喷嘴形成的火焰所点燃,进行气化燃烧反应,预热喷嘴火焰可维持一段时间,待工艺喷嘴火焰完全稳定后再熄灭。火焰熄灭后的预热喷嘴可喷入少量氮气、二氧化碳或者蒸汽等气体对自身进行保护。由于本发明设计的气化炉燃烧室设有多个工艺喷嘴室及其工艺喷嘴,在系统进行投料工作时,可以一对喷嘴投料,也可以两对喷嘴同时投料。The combustion chamber of the gasification furnace designed according to the invention has the characteristics of fast and stable ignition at start-up. Through the preheating nozzle in the preheating nozzle chamber on the top, diesel, natural gas, liquefied petroleum gas, factory bleed gas or other gas and liquid fuels are used for combustion reaction with air. First, the main water-cooled wall coil is preheated, and then The coal-water slurry and oxygen are sprayed through the process nozzle installed in the process nozzle chamber, ignited by the flame formed by the preheating nozzle, and the gasification combustion reaction is carried out. The flame of the preheating nozzle can be maintained for a period of time. After the flame of the process nozzle is completely stable, off. After the flame is extinguished, the preheating nozzle can inject a small amount of nitrogen, carbon dioxide or steam to protect itself. Since the combustion chamber of the gasification furnace designed by the present invention is provided with a plurality of process nozzle chambers and process nozzles, when the system is feeding materials, one pair of nozzles can feed materials, or two pairs of nozzles can feed materials at the same time.
按照本发明设计的气化炉燃烧室,还具有负荷范围宽,调节手段灵活的特点。由于设置了多个工艺喷嘴室及其工艺喷嘴,气化炉燃烧室可以采用所有工艺喷嘴以相同的负荷工作,也可以部分工艺喷嘴工作而其他工艺喷嘴在用少量氮气、二氧化碳或者蒸汽保护的情况下可以停止工作,或者不同位置的工艺喷嘴按照不同负荷工作,通过这些灵活调节手段,可以使整体气化炉在极大的负荷范围内工作。The combustion chamber of the gasification furnace designed according to the invention also has the characteristics of wide load range and flexible adjustment means. Due to the setting of multiple process nozzle chambers and their process nozzles, the combustion chamber of the gasifier can use all process nozzles to work at the same load, or some process nozzles can work while other process nozzles are protected with a small amount of nitrogen, carbon dioxide or steam The gasifier can be stopped working under different conditions, or the process nozzles in different positions work according to different loads. Through these flexible adjustment methods, the overall gasifier can work within a very large load range.
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